US2708203A - Preparation of polymeric titanium organic compounds - Google Patents

Preparation of polymeric titanium organic compounds Download PDF

Info

Publication number
US2708203A
US2708203A US337438A US33743853A US2708203A US 2708203 A US2708203 A US 2708203A US 337438 A US337438 A US 337438A US 33743853 A US33743853 A US 33743853A US 2708203 A US2708203 A US 2708203A
Authority
US
United States
Prior art keywords
polymeric
titanium
acylate
reaction
product
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US337438A
Inventor
John H Haslam
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to US337438A priority Critical patent/US2708203A/en
Application granted granted Critical
Publication of US2708203A publication Critical patent/US2708203A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M1/00Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants
    • C10M1/08Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants with additives
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F7/00Compounds containing elements of Groups 4 or 14 of the Periodic Table
    • C07F7/003Compounds containing elements of Groups 4 or 14 of the Periodic Table without C-Metal linkages
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/121Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of seven or less carbon atoms
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/121Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of seven or less carbon atoms
    • C10M2207/122Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of seven or less carbon atoms monocarboxylic
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/125Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of eight up to twenty-nine carbon atoms, i.e. fatty acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/129Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of thirty or more carbon atoms
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2227/00Organic non-macromolecular compounds containing atoms of elements not provided for in groups C10M2203/00, C10M2207/00, C10M2211/00, C10M2215/00, C10M2219/00 or C10M2223/00 as ingredients in lubricant compositions
    • C10M2227/06Organic compounds derived from inorganic acids or metal salts
    • C10M2227/065Organic compounds derived from inorganic acids or metal salts derived from Ti or Zr
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00Metal present as such or in compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/08Groups 4 or 14
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2050/00Form in which the lubricant is applied to the material being lubricated
    • C10N2050/10Semi-solids; greasy
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S516/00Colloid systems and wetting agents; subcombinations thereof; processes of
    • Y10S516/01Wetting, emulsifying, dispersing, or stabilizing agents
    • Y10S516/06Protein or carboxylic compound containing
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S516/00Colloid systems and wetting agents; subcombinations thereof; processes of
    • Y10S516/905Agent composition per se for colloid system making or stabilizing, e.g. foaming, emulsifying, dispersing, or gelling
    • Y10S516/917The agent contains organic compound containing oxygen
    • Y10S516/918The compound contains carboxylic acid ester group

Definitions

  • This invention pertains to an acidolysis reaction of polymeric titanium and zirconium acylates, and more particularly to novel and improved processes for manufacturing certain polymeric acylates of said metals, the acylate radicals of which are derived from high-boiling carboxylic acids.
  • the direct acylation of ortho esters of titanium by reaction with carboxylic acids causes some condensation and polymerization of the resulting titanium acylate (some times referred to as carboxylate).
  • the direct acylation by the methods of U. S. No. 2,621,193 in particular, and to a lesser degree by those of U. S. No. 2,621,195, produces from high-boiling carboxylic acids reaction product mixtures which are diflicult to purify due to the solubility of the acylating acid in the product. Products made from long chain acids, such as, for example, stearic acid, are even more difficult and expensive to purify because solvent extraction must be resorted to for removal of any unreacted acids or oy-products.
  • the invention comprises intimately commingling for reaction a polymeric titanium acylate 7 with a carboxylic acid having a higher boiling pointthan the carboxylic acid co-product corresponding to the acyl radicals of the original polymeric titanium acylate, removing the coproduct carboxylic acid formed in the reaction by subjecting the reaction products to distillation, and recovering the polymeric titanium acylate product.
  • two moles of a long chain (824 carbon atoms) or high-boiling aliphatic carboxylic acid, such as, for example, stearic acid are suitably commingled and commixed for heating and reaction in a reaction vessel equipped with a distillation head with one mole unit of a polymeric titanium acylate, as for example polymeric titanium propionate having the formula:
  • lower boiling acid co-products can be recycled for reuse in the process to make more of the initial polymeric titanium acylate from a titanium ortho ester.
  • polymeric titanium acylates of high-boiling car- 'boxylic acids of this invention in addition to their usefulness as waxes, can be employed as surface active agents, lubricants, and lubricant additives, etc. They will vary from viscous liquids to waxy solids, depending upon the chain length or configuration or the acyl groups present therein.
  • Example I 176 parts by weight of n-butyric acid was mixed with 284 parts of tetraisopropyl titanate in a distillation type reaction vessel. 1 mole of water was added slowly to the mixture, with good agitation. After the water addition, the temperature of the mixture was raised to 100 C. and 216 parts of isopropanol was distilled ofi and a polymeric titanium butyrate produced which had a few isopropoxy groups (less than /2 mole unit isopropoxy radical per atom of Ti) still remaining attached to the Ti atom. To this polymeric titanium butyrate was added 565 parts of oleic acid with agitation and 186 parts of distillate was then distilled off, of which 164 parts was butyric acid. The reaction product was found to consist essentially of polymeric titanium oleate.
  • Example 11 (CH3)2CHCOO -TlO- OCCIHCHDB OZCixHss it was obtained by distilling off the resultant 2 mole parts of isobutyric acid.
  • the polymeric or condensed titanium or zirconium acylate useful as a starting reactant herein has substantially the general formula:
  • Y and Y in the chain terminating groups comprise an alkyl (methyl, ethyl, propyl, butyl, etc.) or an acyl radical
  • R and R equal a radical selected from the group hydrogen, alkyl, cycloalkyl, aryl radical, alkene or an alkylaryl radical
  • x is greater than 1 and preferably ranges from 2-100.
  • Pr ferably the acylate O O (O&R) and (O i JR) substituent groups are such that in the reaction the exchanged acid evolved or produced therefrom is of relatively low boiling point, e. g., will contain from 2-5 carbon atoms and not more than 8 carbon atoms in its chain.
  • polymeric titanium or zirconium acetate polymeric titani um or zirconium propionate, polymeric titanium or zirconium isobutyrate, and the like
  • polymeric or condensed titanium acylates are especially useful and preferred for employment. They can be readily prepared by reacting an alkyl orthotitanate, such as tetraethyl titanate, with a carboxylic acid and a regulated quantity of water, as contemplated in my U. S. Patent 2,621,195.
  • a mixed titanium acylate hav- 4 ing any desired ratio of acylate groups may be produced.
  • Such mixed titanium acylates can be produced by reacting less than the stoichiometric equivalent of carboxylic acid with the titanium acylate and separating the co-product carboxylic acid from the reaction mixture.
  • Such a a reaction is represented by the equation:
  • the polymer unit being represented by the formula any carboxylic acid boiling higher than n-butyric acid can be used.
  • acids include those containing decanoic, hyptylic, sabacic, caprylic, capric, palmitic, oleic, stearic, lauric, behenic, adipic, benzoic, ortho chlorbenzoic, trichloroacetic, etc.
  • Mixtures of acids such as, for example, those occurring in natural fats and oils, and the like, are also contemplated for use.
  • a wider choice, with regard to boiling point of reactant carboxylic acids, can be used when the co-product carboxylic acid is separated from the product titanium acylate by means other than distillation, as for example fractional crystallization or precipitation of either the coproduct carboxylic acid or the product polymeric titanium acylate.
  • a process for acidolysis of a polymeric group IV metal acylate corresponding to the formula wherein Y and Y are selected from the group consisting of an alkyl and acyl radical, R and R are selected from the group consisting of hydrogen, alkyl, cycloalkyl, aryl, alkene and alkylaryl, and x is a number greater than 1, with a carboxylic acid having a higher boiling point than the carboxylic acid co-product which corresponds to the acyl radical of said polymeric metal acylate reactant, removing by distillation from the reaction mass co-product carboxylic acid formed in the reaction, and recovering the resulting polymeric group IV metal acylate product.
  • a process for producing a polymeric titanium acylate comprising reacting about one mole unit of a polymeric titanium acylate corresponding to the formula:
  • R and R are selected from the group consist ing of an alkyl, cycloalkyl, aryl, alkene and alkylaryl radical, and x is a number greater than 1 with about two moles of a saturated, monocarbcxylic acid having a higher boiling point than the carboxylic acid product of an acyl radical in said acylate reactant, removing by distillation co-product acid formed in the reaction, and recovering the desired polymeric titanium acylate reaction product.
  • a process for the production of polymeric titanium stearate by commingling and reacting in a reaction vessel about two moles parts of stearic acid with one mole part of polymeric titanium butyrate, removing by distillation co-product butyric acid formed in the reaction and recovering the resulting acylate product.
  • a process for the production of polymeric titanium oleate by commingling and reacting in a reaction vessel about two moles parts of oleic acid with one mole party of polymeric titanium butyrate, removing by distillation co-product butyric acid formed in the reaction and recovering the resulting acylate product.
  • a process for the production of polymeric titanium oleate by commingling and reacting in a reaction vessel about two moles parts of oleic acid with one mole part of polymeric titanium propionate, removing by distillation co-product propionic acid formed in the reaction and recovering the resulting acylate product.
  • a process for producing polymeric mixed titanium acylates comprising commingling and reacting a polymeric titanium acylate corresponding to the formula:

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

Unite PREPARATEON 0F PGLYMERIC TITANIUNE GRGANIC COMPOUNDS John H. Haslam, Wilmington, DeL, assignor to E. I. du Pont de Nernours and Company, Wilmington, Del. a corporation of Delaware No Drawing. Application February 17, 1953, Serial No. 337,438
7 Claims. (Cl. 260-414) This invention pertains to an acidolysis reaction of polymeric titanium and zirconium acylates, and more particularly to novel and improved processes for manufacturing certain polymeric acylates of said metals, the acylate radicals of which are derived from high-boiling carboxylic acids.
The direct acylation of ortho esters of titanium by reaction with carboxylic acids causes some condensation and polymerization of the resulting titanium acylate (some times referred to as carboxylate). The direct acylation, by the methods of U. S. No. 2,621,193 in particular, and to a lesser degree by those of U. S. No. 2,621,195, produces from high-boiling carboxylic acids reaction product mixtures which are diflicult to purify due to the solubility of the acylating acid in the product. Products made from long chain acids, such as, for example, stearic acid, are even more difficult and expensive to purify because solvent extraction must be resorted to for removal of any unreacted acids or oy-products.
It is among the objects of this invention to overcome these and other disadvantages in polymeric Group IV metal acylate manufacture, and to provide, in particular, a new acyl radical exchange reaction of polymeric titanium and zirconium acylates. A further object 'is to provide an improved, direct process for the manufacture of organic solvent-soluble, relatively pure polymeric acylates of titanium and zirconium of relatively high-boiling carboxylic acids. Other objects will be apparent from the ensuing description.
These objects are accomplished herein by mixing and reacting a polymeric group IV metal acylate with a carboxylic acid and separating the acylate product from the co-product carboxylic acid formed from the exchanged acyl radical of the initial polymeric acylate.
More specifically, the invention comprises intimately commingling for reaction a polymeric titanium acylate 7 with a carboxylic acid having a higher boiling pointthan the carboxylic acid co-product corresponding to the acyl radicals of the original polymeric titanium acylate, removing the coproduct carboxylic acid formed in the reaction by subjecting the reaction products to distillation, and recovering the polymeric titanium acylate product.
In one preferred adaptation of the invention, two moles of a long chain (824 carbon atoms) or high-boiling aliphatic carboxylic acid, such as, for example, stearic acid, are suitably commingled and commixed for heating and reaction in a reaction vessel equipped with a distillation head with one mole unit of a polymeric titanium acylate, as for example polymeric titanium propionate having the formula:
0 (i) l C 2H5] TiO- I 11.02000 OCCaHt mula:
i O (J) 0 H351 if desired, lower boiling acid co-products can be recycled for reuse in the process to make more of the initial polymeric titanium acylate from a titanium ortho ester.
The polymeric titanium acylates of high-boiling car- 'boxylic acids of this invention, in addition to their usefulness as waxes, can be employed as surface active agents, lubricants, and lubricant additives, etc. They will vary from viscous liquids to waxy solids, depending upon the chain length or configuration or the acyl groups present therein.
To a clearer understanding of the invention, the following examples are given. These are merely in illustration and not in limitation of the invention.
Example I 176 parts by weight of n-butyric acid was mixed with 284 parts of tetraisopropyl titanate in a distillation type reaction vessel. 1 mole of water was added slowly to the mixture, with good agitation. After the water addition, the temperature of the mixture was raised to 100 C. and 216 parts of isopropanol was distilled ofi and a polymeric titanium butyrate produced which had a few isopropoxy groups (less than /2 mole unit isopropoxy radical per atom of Ti) still remaining attached to the Ti atom. To this polymeric titanium butyrate was added 565 parts of oleic acid with agitation and 186 parts of distillate was then distilled off, of which 164 parts was butyric acid. The reaction product was found to consist essentially of polymeric titanium oleate.
Example 11 (CH3)2CHCOO -TlO- OCCIHCHDB OZCixHss it was obtained by distilling off the resultant 2 mole parts of isobutyric acid.
While the invention has been described as applied to certain specific embodiments thereof, it is not restricted thereto. Hence, due variance therefrom can be resorted to without departing from its underlying principles and scope. Thus, the polymeric or condensed titanium or zirconium acylate useful as a starting reactant herein has substantially the general formula:
wherein Y and Y in the chain terminating groups comprise an alkyl (methyl, ethyl, propyl, butyl, etc.) or an acyl radical, R and R equal a radical selected from the group hydrogen, alkyl, cycloalkyl, aryl radical, alkene or an alkylaryl radical, and x is greater than 1 and preferably ranges from 2-100. Pr ferably the acylate O O (O&R) and (O i JR) substituent groups are such that in the reaction the exchanged acid evolved or produced therefrom is of relatively low boiling point, e. g., will contain from 2-5 carbon atoms and not more than 8 carbon atoms in its chain. Among examples of preferred useful polymeric acylates, polymeric titanium or zirconium acetate, polymeric titani um or zirconium propionate, polymeric titanium or zirconium isobutyrate, and the like, can be mentioned. The polymeric or condensed titanium acylates are especially useful and preferred for employment. They can be readily prepared by reacting an alkyl orthotitanate, such as tetraethyl titanate, with a carboxylic acid and a regulated quantity of water, as contemplated in my U. S. Patent 2,621,195. Thus, as disclosed in that patent, to one mole of an ortho ester of titanium there can be added about two moles of a monocarboxylic acid and controlled addition then effected of about one mole water per atom of titanium, followed by heating of the reactants until the desired polymeric polytitanic ester is formed. Alternatively, the methods disclosed in U. S. Patent 2,621,193 can be utilized in effecting such preparation. The product of such reactions, depending on the exact quantities of reactants, will contain a small amount of residual alkoXy radical, in the terminal group for example, not completely removed by the acylation reaction. Furthermore, by reacting the proper quantity of carboxylic acid with the titanium acylate, a mixed titanium acylate hav- 4 ing any desired ratio of acylate groups may be produced. Such mixed titanium acylates can be produced by reacting less than the stoichiometric equivalent of carboxylic acid with the titanium acylate and separating the co-product carboxylic acid from the reaction mixture. Such a a reaction is represented by the equation:
point than the exchangeable acyl radical of the original titanium or zirconium acylate in the acid form. For example, in the case where the original compound is polymeric titanium butyrate, the polymer unit being represented by the formula any carboxylic acid boiling higher than n-butyric acid can be used. Examples of such acids include those containing decanoic, hyptylic, sabacic, caprylic, capric, palmitic, oleic, stearic, lauric, behenic, adipic, benzoic, ortho chlorbenzoic, trichloroacetic, etc. Mixtures of acids, such as, for example, those occurring in natural fats and oils, and the like, are also contemplated for use. A wider choice, with regard to boiling point of reactant carboxylic acids, can be used when the co-product carboxylic acid is separated from the product titanium acylate by means other than distillation, as for example fractional crystallization or precipitation of either the coproduct carboxylic acid or the product polymeric titanium acylate.
While specific temperatures have been mentioned and utilized herein, the invention is not to be construed as restricted thereto. In general, use is contemplated of any temperature designed to control and effect the desired reaction and the subsequent recovery, by distillation, of the acylating acid which is displaced. If desired, recourse can be had to any convenient and desired pressure during the distillation.
I claim as my invention:
1. A process for acidolysis of a polymeric group IV metal acylate corresponding to the formula wherein Y and Y are selected from the group consisting of an alkyl and acyl radical, R and R are selected from the group consisting of hydrogen, alkyl, cycloalkyl, aryl, alkene and alkylaryl, and x is a number greater than 1, with a carboxylic acid having a higher boiling point than the carboxylic acid co-product which corresponds to the acyl radical of said polymeric metal acylate reactant, removing by distillation from the reaction mass co-product carboxylic acid formed in the reaction, and recovering the resulting polymeric group IV metal acylate product.
3. A process for producing a polymeric titanium acylate comprising reacting about one mole unit of a polymeric titanium acylate corresponding to the formula:
wherein R and R are selected from the group consist ing of an alkyl, cycloalkyl, aryl, alkene and alkylaryl radical, and x is a number greater than 1 with about two moles of a saturated, monocarbcxylic acid having a higher boiling point than the carboxylic acid product of an acyl radical in said acylate reactant, removing by distillation co-product acid formed in the reaction, and recovering the desired polymeric titanium acylate reaction product.
4. A process for the production of polymeric titanium stearate, by commingling and reacting in a reaction vessel about two moles parts of stearic acid with one mole part of polymeric titanium butyrate, removing by distillation co-product butyric acid formed in the reaction and recovering the resulting acylate product.
5. A process for the production of polymeric titanium oleate, by commingling and reacting in a reaction vessel about two moles parts of oleic acid with one mole party of polymeric titanium butyrate, removing by distillation co-product butyric acid formed in the reaction and recovering the resulting acylate product.
6. A process for the production of polymeric titanium oleate, by commingling and reacting in a reaction vessel about two moles parts of oleic acid with one mole part of polymeric titanium propionate, removing by distillation co-product propionic acid formed in the reaction and recovering the resulting acylate product.
7. A process for producing polymeric mixed titanium acylates comprising commingling and reacting a polymeric titanium acylate corresponding to the formula:
References Cited in the file of this patent UNITED STATES PATENTS Boyd Oct. 14, 1952 2,621,194 Balthis Dec. 9, 1952 2,621,195 Haslam Dec. 9, 1952

Claims (1)

1. A PROCESS FOR ACIDOLYSIS OF A POLYMERIC GROUP IV METAL ACYLATE CORRESPONDING TO THE FORMULA
US337438A 1953-02-17 1953-02-17 Preparation of polymeric titanium organic compounds Expired - Lifetime US2708203A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US337438A US2708203A (en) 1953-02-17 1953-02-17 Preparation of polymeric titanium organic compounds

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US337438A US2708203A (en) 1953-02-17 1953-02-17 Preparation of polymeric titanium organic compounds

Publications (1)

Publication Number Publication Date
US2708203A true US2708203A (en) 1955-05-10

Family

ID=23320540

Family Applications (1)

Application Number Title Priority Date Filing Date
US337438A Expired - Lifetime US2708203A (en) 1953-02-17 1953-02-17 Preparation of polymeric titanium organic compounds

Country Status (1)

Country Link
US (1) US2708203A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2916392A (en) * 1958-04-07 1959-12-08 Monsanto Chemicals Air drying films from unsaturated fatty acid metal salts
US2985604A (en) * 1957-03-05 1961-05-23 Union Carbide Corp Shaped resins
US2985607A (en) * 1957-03-05 1961-05-23 Union Carbide Corp Rubber additives
US2989412A (en) * 1956-04-17 1961-06-20 Union Carbide Corp Organometallic pigment dispersants based on acylates polyhydric alcoholates and aminoalcoholates of group iv-b metals
US3098041A (en) * 1961-11-20 1963-07-16 Union Carbide Corp Lubricating composition
US3180741A (en) * 1960-11-29 1965-04-27 Horizons Inc Liquid polymers, solid articles made therefrom and methods of preparing same
US3243447A (en) * 1960-10-31 1966-03-29 Rinse Jacobus Preparation of spacial tetrameric acyloxy group iv metal oxides
EP0625564A1 (en) * 1993-05-18 1994-11-23 INDIAN OIL CORPORATION Ltd. Lubricating oil

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2614112A (en) * 1951-01-30 1952-10-14 Monsanto Chemicals Polymeric titanium mixed esters
US2621195A (en) * 1950-10-26 1952-12-09 Du Pont Polymeric titanium compounds
US2621194A (en) * 1950-07-26 1952-12-09 Du Pont Polymeric hydroxyl-containing titanium carboxylates and methods for preparing same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2621194A (en) * 1950-07-26 1952-12-09 Du Pont Polymeric hydroxyl-containing titanium carboxylates and methods for preparing same
US2621195A (en) * 1950-10-26 1952-12-09 Du Pont Polymeric titanium compounds
US2614112A (en) * 1951-01-30 1952-10-14 Monsanto Chemicals Polymeric titanium mixed esters

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2989412A (en) * 1956-04-17 1961-06-20 Union Carbide Corp Organometallic pigment dispersants based on acylates polyhydric alcoholates and aminoalcoholates of group iv-b metals
US2985604A (en) * 1957-03-05 1961-05-23 Union Carbide Corp Shaped resins
US2985607A (en) * 1957-03-05 1961-05-23 Union Carbide Corp Rubber additives
US2916392A (en) * 1958-04-07 1959-12-08 Monsanto Chemicals Air drying films from unsaturated fatty acid metal salts
US3243447A (en) * 1960-10-31 1966-03-29 Rinse Jacobus Preparation of spacial tetrameric acyloxy group iv metal oxides
US3180741A (en) * 1960-11-29 1965-04-27 Horizons Inc Liquid polymers, solid articles made therefrom and methods of preparing same
US3098041A (en) * 1961-11-20 1963-07-16 Union Carbide Corp Lubricating composition
EP0625564A1 (en) * 1993-05-18 1994-11-23 INDIAN OIL CORPORATION Ltd. Lubricating oil

Similar Documents

Publication Publication Date Title
US2621193A (en) Polymeric titanium compounds
US2621195A (en) Polymeric titanium compounds
DE3781886T2 (en) METHOD FOR PRODUCING A POLYSILOXANE CONTAINING ACRYLATE OR METHACRYLATE GROUPS.
US2708203A (en) Preparation of polymeric titanium organic compounds
US2681922A (en) Polymeric zirconium compounds and method of preparing same
US4112235A (en) Transesterification of carboxylic acids
US3032570A (en) Organic titanium compounds
US1993738A (en) Myristyl esters of polycarboxylic acids
US2603616A (en) Plastic compositions and process for producing the same
CS209884B2 (en) Method of preparation of the organo-stannate derivatives of the mercapto-alcanole esters
JPS60233035A (en) Synthesis of vinyl ester
DE890792C (en) Process for the preparation of carboxylic acid esters
US3019247A (en) New organotin derivatives
US3313843A (en) Preparation of cinnamate esters
US4609755A (en) Synthesis of vinyl esters
DE2749083C2 (en) Process for the preparation of organotin compounds
US3071607A (en) Vinyllead compounds
DE1248046B (en) Process for the preparation of acyloxyorganodisiloxanes
US3293283A (en) Process for transesterifying lower alkyl acrylates
GB2075020A (en) Process for the production of carboxylic amides
US2861098A (en) Production of carboxylic acid esters
US2980719A (en) Reaction of titanium esters with acid anhydrides
US3030320A (en) Organic titanium compounds
US2532018A (en) Plasticized resin compositions
US2948743A (en) Oxo-aluminum acylates, alkoxides and phenoxides